CN204154144U - A kind of fermentation tank vapour-recovery unit - Google Patents
A kind of fermentation tank vapour-recovery unit Download PDFInfo
- Publication number
- CN204154144U CN204154144U CN201420542248.6U CN201420542248U CN204154144U CN 204154144 U CN204154144 U CN 204154144U CN 201420542248 U CN201420542248 U CN 201420542248U CN 204154144 U CN204154144 U CN 204154144U
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- pipeline
- fermentation tank
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- water cylinder
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Abstract
The utility model discloses a kind of fermentation tank vapour-recovery unit, belong to Steam Recovery technology technical field.Comprise fermentation tank and steam-water separator, the pipeline being separated valve between described fermentation tank and steam-water separator by being equipped with carbonated drink is connected; Also comprise hot-water cylinder and circulating pump, the heating tube that injector is equipped with in upper end is set up in described hot-water cylinder, pipeline between described fermentation tank and carbonated drink separation valve is provided with branched pipe and is connected by pipeline with the left hole of injector by Steam Recovery valve, be connected by pipeline between the output port of described circulating pump and the upper hole of injector, the input port of circulating pump is connected by pipeline with hot-water cylinder.The utility model can reclaim fermentation tank sterilisation vapour effectively, and the rate of recovery can reach more than 70%.Equipment investment is few, and structure is simple, and convenience easy to maintenance, has high economic benefit.
Description
Technical field
The utility model relates to Steam Recovery technology technical field.
Background technology
Steam is often used to carry out disinfection to fermentation tank, material in the industry production such as current biology, pharmacy, actual use procedure first carries out sky with saturated vapor to fermentation slack tank to disappear, about 1.5 hours are passed in clean fermentation tank by saturated vapor, then the material (culture medium) prepared is made to enter in fermentation tank by pipeline, pass into a large amount of steam again to about heating material to 120 DEG C, then continue pressurize about 50 minutes with steam.This process will have a large amount of steam to be entered discharged in air after steam-water separator by valve, and its temperature, still more than 100 DEG C, causes a large amount of waste hot gas to waste, and can pollute atmospheric environment.Under the current energy more and more intense situation, these energy recovery have high economic worth and social effect.These heat energy from waste gas are equivalent to consume 10% of heat energy in production, reclaim energy-saving effect clearly to it.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of fermentation tank vapour-recovery unit, have simple and practical, facilitate waste gas recovery, energy-saving effect outstanding feature.
For solving the problems of the technologies described above, technical solution adopted in the utility model is: a kind of fermentation tank vapour-recovery unit, comprises fermentation tank and steam-water separator, and the pipeline being separated valve between described fermentation tank and steam-water separator by being equipped with carbonated drink is connected; Also comprise hot-water cylinder and circulating pump, the heating tube that injector is equipped with in upper end is set up in described hot-water cylinder, pipeline between described fermentation tank and carbonated drink separation valve is provided with branched pipe and is connected by pipeline with the left hole of injector by Steam Recovery valve, be connected by pipeline between the output port of described circulating pump and the upper hole of injector, the input port of circulating pump is connected by pipeline with hot-water cylinder.
To the further improvement that the utility model does be: also comprise heat-exchanger pump and filling pipe; The input port of described heat-exchanger pump is connected by pipeline with hot-water cylinder, and the output port of heat-exchanger pump is connected with hot water user pipe by valve; Described filling pipe is arranged on hot-water cylinder.Pipeline on pipeline on pipeline between heat-exchanger pump and hot-water cylinder, between described circulating pump and injector and between circulating pump and hot-water cylinder is equipped with valve respectively.
The beneficial effect adopting technique scheme to produce is: the utility model can reclaim fermentation sterilisation vapour effectively, and the rate of recovery can reach more than 70%.Equipment investment is little, and structure is simple, and convenience easy to maintenance, has high economic benefit.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
As shown in the figure: 1 Steam Recovery valve, 2 carbonated drinks are separated valve, 3 injectors, 4 filling pipes, 5 heating tubes, 6 circulating pumps, 7 hot-water cylinders, 8 heat-exchanger pumps, 9 hot water user pipes, 10 steam-water separators, 11 fermentation tanks.Detailed description of the invention
Contrast Fig. 1 uses step to be described further to operation of the present utility model: a kind of fermentation tank vapour-recovery unit, comprise fermentation tank 11 and steam-water separator 10, the pipeline being separated valve 2 between described fermentation tank 11 and steam-water separator 10 by being equipped with carbonated drink is connected; Also comprise hot-water cylinder 7 and circulating pump 6, the heating tube 5 that injector 3 is equipped with in upper end is set up in described hot-water cylinder 7, pipeline between described fermentation tank 11 and carbonated drink separation valve 2 is provided with branched pipe and is connected by pipeline by the left hole of Steam Recovery valve 1 with injector 3, be connected by pipeline between the output port of described circulating pump 6 and the upper hole of injector 3, the input port of circulating pump 6 is connected by pipeline with hot-water cylinder 7.Also comprise heat-exchanger pump 8 and filling pipe 4; The input port of described heat-exchanger pump 8 is connected by pipeline with hot-water cylinder 7, and the output port of heat-exchanger pump 8 is connected with hot water user pipe 9 by valve; Described filling pipe 4 is arranged on hot-water cylinder 7.Pipeline on pipeline on pipeline between heat-exchanger pump 8 and hot-water cylinder 7, between described circulating pump 6 and injector 3 and between circulating pump 6 and hot-water cylinder 7 is equipped with valve respectively.
The utility model is by installing Steam Recovery valve 1, the exhaust steam of fermentation tank 11 steam is introduced injector 3, steam-water mixing is realized in injector 3, thus steam is fully dissolved in hot-water cylinder 7, circulated by circulating pump 6, heat-exchanger pump 8 leads to user, or as thermal water source or for winter heating.
Claims (2)
1. a fermentation tank vapour-recovery unit, comprise fermentation tank (11) and steam-water separator (10), the pipeline being separated valve (2) between described fermentation tank (11) and steam-water separator (10) by being equipped with carbonated drink is connected, it is characterized in that: also comprise hot-water cylinder (7), heat-exchanger pump (8), filling pipe (4) and circulating pump (6), the heating tube (5) that injector (3) are equipped with in upper end is set up in described hot-water cylinder (7), pipeline between described fermentation tank (11) and carbonated drink separation valve (2) is provided with branched pipe and is connected by pipeline by the left hole of Steam Recovery valve (1) with injector (3), the output port of described circulating pump (6) is connected by pipeline with between the upper hole of injector (3), the input port of circulating pump (6) is connected by pipeline with hot-water cylinder (7), the input port of described heat-exchanger pump (8) is connected by pipeline with hot-water cylinder (7), the output port of heat-exchanger pump (8) is managed (9) by valve with hot water user and is connected, described filling pipe (4) is arranged on hot-water cylinder (7).
2. a kind of fermentation tank vapour-recovery unit according to claim 1, is characterized in that: the pipeline on the pipeline on the pipeline between heat-exchanger pump (8) and hot-water cylinder (7), between described circulating pump (6) and injector (3) above and between circulating pump (6) and hot-water cylinder (7) is equipped with valve respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420542248.6U CN204154144U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank vapour-recovery unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420542248.6U CN204154144U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank vapour-recovery unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204154144U true CN204154144U (en) | 2015-02-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420542248.6U Expired - Fee Related CN204154144U (en) | 2014-09-17 | 2014-09-17 | A kind of fermentation tank vapour-recovery unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204154144U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106959023A (en) * | 2017-05-16 | 2017-07-18 | 安徽金星钛白（集团）有限公司 | A kind of titanium white flour flow design air-flow crushing tail gas secondary waste heat recycling system |
| CN107131775A (en) * | 2017-05-16 | 2017-09-05 | 安徽金星钛白（集团）有限公司 | A kind of titanium dioxide processing air-flow crushing waste heat from tail gas Application way |
-
2014
- 2014-09-17 CN CN201420542248.6U patent/CN204154144U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106959023A (en) * | 2017-05-16 | 2017-07-18 | 安徽金星钛白（集团）有限公司 | A kind of titanium white flour flow design air-flow crushing tail gas secondary waste heat recycling system |
| CN107131775A (en) * | 2017-05-16 | 2017-09-05 | 安徽金星钛白（集团）有限公司 | A kind of titanium dioxide processing air-flow crushing waste heat from tail gas Application way |
| CN107131775B (en) * | 2017-05-16 | 2019-06-25 | 安徽金星钛白（集团）有限公司 | A kind of processing of titanium dioxide utilizes method with air-flow crushing waste heat from tail gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150211 Termination date: 20170917 |